EP0649842B1 - Process for preparing derivatives of (halo)amino compounds by carbonylation - Google Patents
Process for preparing derivatives of (halo)amino compounds by carbonylation Download PDFInfo
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- EP0649842B1 EP0649842B1 EP94116269A EP94116269A EP0649842B1 EP 0649842 B1 EP0649842 B1 EP 0649842B1 EP 94116269 A EP94116269 A EP 94116269A EP 94116269 A EP94116269 A EP 94116269A EP 0649842 B1 EP0649842 B1 EP 0649842B1
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- palladium
- carbon monoxide
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
- C07D251/40—Nitrogen atoms
- C07D251/54—Three nitrogen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
- C07D251/40—Nitrogen atoms
- C07D251/54—Three nitrogen atoms
- C07D251/66—Derivatives of melamine in which a hetero atom is directly attached to a nitrogen atom of melamine
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
- C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
- C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
- C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
- C07D251/40—Nitrogen atoms
- C07D251/54—Three nitrogen atoms
- C07D251/70—Other substituted melamines
Definitions
- the present invention relates to a process for preparing derivatives of (halo)amino compounds by carbonylation.
- carbamate functional 1,3,5-triazines which are disclosed in US-A-4,939,213, US-A-5,084,541, US-A-5,288,865, EP-A-0604922 and EP-0624577.
- carbamate functional 1,3,5-triazines disclosed in these references have been found to be particularly useful as crosslinkers in coating compositions based upon hydroxy functional resins, with the cured coatings possessing a wide range of desirable properties.
- This invention relates to the preparation of isocyanate and carbamate functional derivatives of optionally halogenated amino-1,3,5-triazines via carbonylation using carbon monoxide and a metal promoter for promoting carbonylation.
- isocyanate functional 1,3,5-triazines can be produced without many of the disadvantages of the prior art processes by the carbonylation of (halo)amino-1,3,5-triazines with carbon monoxide in the presence of a metal promoter for promoting carbonylation.
- isocyanate functional 1,3,5-triazines may be readily converted to the carbamate counterparts either by carrying out the carbonylation in the presence of a hydroxy compound or by adding the hydroxy compound to the isocyanate functional 1,3,5-triazine without isolating it.
- the 1,3,5-triazine contains an amino group or a mixed haloamino group to be carbonylated, it is preferred that an oxidant system be present in an amount sufficient to restore the metal promoter to a promotively effective oxidation state.
- an oxidant system be present in an amount sufficient to restore the metal promoter to a promotively effective oxidation state.
- a hydrogen halide acceptor be present in an amount sufficient to neutralize the hydrohalide by-product of the carbonylation.
- the 1,3,5-triazine carbonylated product produced by contacting (a), (b), and (c) is an isocyanate functional 1,3,5-triazine.
- a carbamate functional 1,3,5-triazine derivative can readily be produced by one of two routes - (i) reacting components (a), (b), (c) in the presence of a hydroxy compound, or (ii) by post-reacting the isocyanate 1,3,5-triazine derivative with such a hydroxy compound.
- the advantages of the present process include, for example:
- the present invention is a process for preparing carbonylated 1,3,5-triazine derivatives via the carbonylation of (halo)amino group-containing 1,3,5-triazines.
- (halo)amino group-containing 1,3,5-triazine refers to 1,3,5-triazine compounds containing at least one of an amino group (-NH 2 ), mixed haloamino group (-NH(Hal)) and/or fully haloamino group (-N(Hal) 2 ) as a substituent attached to the 1,3,5-triazine core.
- a "carbonylated product” or a “carbonylated derivative,” in the context of the present invention, refers to a 1,3,5-triazine product with a substituent containing a carbonyl (C O) group which has been introduced via carbonylation.
- the fully carbonylated product of melamine (2,4,6-triisocyanato-1,3,5-triazine) is a carbonylated product in the context of the present invention, as are the carbamate derivatives thereof (such as 2,4,6-tris-(methoxycarbonylamino)-1,3,5-triazine).
- Another related example of a carbonylated product in the context of the present invention is 2,4,6-tris-(chlorocarbonylamino)-1,3,5-triazine.
- the process of the present invention includes the use of carbon monoxide and a metal catalyst system containing a metal promoter for promoting carbonylation of the (halo)amino groups for converting them to an isocyanate.
- a metal catalyst system containing a metal promoter for promoting carbonylation of the (halo)amino groups for converting them to an isocyanate.
- carbamate functional 1,3,5-triazine is at least bis-functional
- a crosslinking agent and/or reactive modifier usable with polyfunctional active hydrogen containing resins, such as hydroxyfunctional acrylic or polyester resins, for producing curable compositions which have utility in coatings, adhesives, molding, and other applications, as disclosed in the previously incorporated commonly owned references.
- 1,3,5-triazine suitable for use in the process of the present invention is a (halo)amino group-containing 1,3,5-triazine represented by the formula: wherein
- hydrocarbyl in the context of the present invention, is a group which contains carbon and hydrogen atoms and includes, for example, alkyl, aryl, aralkyl, alkenyl.
- hydrocarbylene refers to a divalent hydrocarbyl such as, for example, alkylene, arylene, aralkylene, alkenylene, and substituted derivatives thereof.
- the preferred melamines are those wherein each Q 1 is independently selected from hydrogen and halogen, more preferably hydrogen and chlorine.
- each Q 1 is independently selected from hydrogen and halogen, more preferably hydrogen and chlorine.
- melamine Q and Q 1 are all hydrogen
- N,N',N''-trichloromelamine one of the Q groups is hydrogen and the other is chlorine, and one Q 1 group on each of the remaining nitrogens is hydrogen while the other is chlorine
- hexachloromelamine Q and Q 1 are all chlorine.
- the preferred guanamines are those represented by the above general formula wherein Z 1 is more preferably selected from the group consisting of an alkyl of 1 to 20 carbon atoms, alkenyl of 3 to 20 carbon atoms, aryl of 6 to 20 carbon atoms, and aralkyl of 7 to 20 carbon atoms; and each Q 1 is independently selected from hydrogen and halogen, more preferably hydrogen and chlorine.
- Z 1 is more preferably selected from the group consisting of an alkyl of 1 to 20 carbon atoms, alkenyl of 3 to 20 carbon atoms, aryl of 6 to 20 carbon atoms, and aralkyl of 7 to 20 carbon atoms; and each Q 1 is independently selected from hydrogen and halogen, more preferably hydrogen and chlorine.
- acetoguanamine ethylcarboguanamine, cyclohexylcarboguanamine, benzoguanamine, the N,N'-dichloro derivatives thereof, and N,N,N',N
- the carbon monoxide which can be employed in the present invention may be pure carbon monoxide or may contain other gases such as, for example, nitrogen, argon, helium, carbon dioxide, a hydrocarbon or a halogenated hydrocarbon. Generally, any commercially available carbon monoxide may be utilized; however, it is preferred that the carbon monoxide be substantially free of water for the reasons discussed further below.
- any metal catalyst system containing a metal promoter capable of promoting carbonylation of the (halo)amino groups of the 1,3,5-triazine is usable in the process of the present invention.
- the metal promoter is a group VIII or group I-B metal or a compound containing a group VIII or group I-B metal, including mixtures and complexes thereof, such as disclosed in a number of the previously incorporated references. More preferably, the metal promoter is a compound containing a metal selected from the group consisting of copper, palladium, platinum, ruthenium, rhodium and mixtures thereof, and especially the oxides, halides and organic acid salts of these metals.
- copper (0), palladium (0) and palladium compounds selected from the group consisting of palladium (II) chloride, palladium (II) bromide, palladium (II) acetate, palladium (II) acetyl acetonate, palladium (II) oxide, and mixtures thereof.
- the metal catalyst system may comprise a complex of the metal promoter with one or more ligands.
- the complex is first prepared and thereafter added to the reaction mixture or, alternatively, it is prepared in situ by addition of an uncomplexed metal compound and one or more ligands to the reaction mixture to form a complex thereof prior to carbonylation.
- Ligands commonly used to complex metals are suitable for use in this manner and include, for example, nitrile group containing ligands and carbon monoxide. When the ligand used is a nitrile group containing compound, it may be used as the reaction medium.
- the reaction medium in this case is a solvent for the ingredients of the mixture, and preferably a nitrile solvent selected from the group consisting of acetonitrile, propionitrile, butyronitrile, valeronitrile, benzyl nitrile, benzonitrile, and mixtures thereof.
- a nitrile solvent selected from the group consisting of acetonitrile, propionitrile, butyronitrile, valeronitrile, benzyl nitrile, benzonitrile, and mixtures thereof.
- any oxidant system capable of restoring the metal promotor to a promotively effective oxidation state is usable in the present invention as the oxidant system.
- the oxidant system typically comprises an ingredient or a plurality of ingredients capable of accepting an electron from the metal promoter, thereby restoring it to a promotively effective oxidation state for carrying out the carbonylation reaction.
- the preferred oxidant system is selected from the group consisting of a copper (II) salt, an alkali metal iodide/oxygen couple, molecular oxygen, hydroquinones, dialkyl peroxides and other compounds containing reducible oxygen, including mixtures of the above.
- hydrogen halides are produced as by-products of the carbonylation.
- the presence of hydrogen halides is undesirable due to their noxious and corrosive nature.
- it is preferred to conduct the reaction in the presence of a hydrogen halide acceptor more preferably weak organic or inorganic bases such as, for example, alkali metal phosphates, alkaline earth metal phosphates, alkali metal carboxylates and alkali metal carbonates.
- a hydrogen halide acceptor more preferably weak organic or inorganic bases such as, for example, alkali metal phosphates, alkaline earth metal phosphates, alkali metal carboxylates and alkali metal carbonates.
- Especially preferred hydrogen halide acceptors include calcium phosphate, potassium hydrogen phosphate, sodium phosphate dibasic, sodium acetate and potassium acetate.
- carbamate functional 1,3,5-triazine derivatives can readily be produced in accordance with the present invention by one of two routes - (i) reacting the above-described components in the presence of a hydroxy compound, or (ii) by post-reacting the isocyanate 1,3,5-triazine derivative with such hydroxy compound.
- hydroxy compounds are suitable for use in forming carbamates, and are described in detail in the previously incorporated references. As preferred examples may be mentioned alcohols and phenols.
- alcohols may be mentioned, for example, straight or branched monohydric or polyhydric alkanols and alkenols having 1 to 20 carbon atoms per molecule, monohydric or polyhydric cycloalkanols and cycloalkenols having 3 to 20 carbon atoms in the molecule, and monohydric and polyhydric aralalkyls having 7 to 20 carbon atoms per molecule.
- these alcohols may also have a substituent such as a halogen atom, a cyano group, an alkoxy group, a sulfoxide group, a sulfone group, a carbonyl group, an ester group, an ether group and an amide group. Mixtures of the above are also suitable.
- alcohols may be mentioned aliphatic linear, cyclic, saturated, or unsaturated alcohols having 1 to 8 carbon atoms, as well as mixtures thereof.
- phenol As suitable phenols may be mentioned phenol, various alkyl phenols, various alkoxy phenols, various halogenated phenols, dihydroxybenzene, 4,4-dihydroxydiphenylmethane, various bisphenols such as bisphenol-A, and hydroxynaphthalenes.
- phenol 2-methyl phenol, 3-methyl phenol, 4-methyl phenol, 2-chlorophenol, 3-chlorophenol, 4-chlorophenol, catechol, resorcinol, hydroquinone, and mixtures thereof.
- the components of the reaction mixture are contacted at a temperature, carbon monoxide pressure, and length of time sufficient to carbonylate at least a portion of the (halo)amino groups of the 1,3,5-triazine.
- the carbonylation temperature may vary widely, but is typically in the range of from about 20°C to about 180°C.
- the carbonylation pressure may also vary widely, but is typically in the range of from atmospheric to about 96.6 bar gauge (about 1400 psig), with pressures of from about 48.3 bar gauge (about 700 psig) to about 75.9 bar gauge (about 1100 psig) being preferred.
- the actual carbon monoxide pressure may be slightly lower due to the presence of gaseous inerts in the carbon monoxide stream.
- the length of time for carbonylation again may vary widely, but is typically in the range of from about 2 hours to about 96 hours.
- the metal catalyst system is preferably utilized in catalytic amounts, typically ranging from about 0.01 to about 10 mole% metal promoter, and preferably from about 0.1 to about 3 mole% metal promoter, based upon the number of moles of (halo)amino groups in the 1,3,5-triazines to be carbonylated.
- the oxidant system when required, is preferably present in a sufficient amount to promote the carbonylation of the amino and mixed haloamino groups.
- the oxidant system will be present in an at least stoichiometric amount based upon the number of H atoms present in the amino and mixed haloamino groups.
- the hydrogen halide acceptor when required, is preferably present in an amount to substantially fully neutralize any hydrogen halide by-product from the carbonylation of the mixed and fully haloamino groups of the 1,3,5-triazines.
- the carbonylation is preferably conducted in the presence of solvents such as, for example, aromatic hydrocarbons such as benzene, toluene, xylene and mesitylene; nitriles such as acetonitrile, propionitrile, butyronitrile, valeronitrile, benzyl nitrile and benzonitrile; sulfones such as sulforane, methylsulforane and dimethylsulforane; ethers such as tetrahydrofuran, 1,4-dioxane, 1,2-dimethoxyethane, glyme, diglyme and triglyme; ketones such as acetone and methyl ethyl ketone; esters such as ethyl acetate and ethyl benzoate; amides such as N,N-dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidone and hexamethyl
- haloamino-1,3,5-triazines may be incompatible when haloamino-1,3,5-triazines are carbonylated due to their potential reactivity with such haloamino-1,3,5-triazines, and should be avoided under conidtions where such reactivity may become a concern.
- the preferred solvents are the nitriles and hydroxy compounds.
- the carbonylation may be carried out in the presence of a hydroxy compound (both a reactant and solvent), or the hydroxy compound may be added subsequent to the carbonylation.
- a hydroxy compound both a reactant and solvent
- the amount of hydroxy compound added will vary depending upon the desired degree of carbamate formation. Typically, for full conversion to carbamate functionality, a stoichiometric excess (based upon isocyanate formation) should be utilized.
- a well-known urethanation catalyst may also be added.
- the reaction is preferred to conduct the reaction in the presence of an alcohol/cosolvent system.
- the alcohol/cosolvent ratio can vary widely, but generally should be in the range of about 2/1 to about 10/1.
- the preferred cosolvent is a nitrile solvent.
- a dehydrating additive such as, for example, zeolites, orthoesters, ketals, acetals, enolethers and trialkyl orthoborates.
- a glass-lined, two-liter, stainless steel Zipperclave was charged with the following:
- the reactor and reaction mixture were purged with nitrogen.
- the reactor was pressurized to about 41.4 bar gauge (600 psig) with carbon monoxide at room temperature.
- the reaction temperature was brought to ca. 100°C, and the system was further pressurized to about 55.2 bar gauge (800 psig) with carbon monoxide.
- the reaction mixture was stirred under these conditions for 24 hours.
- the reactor was cooled to room temperature, and the carbon monoxide pressure vented. Nitrogen purge cycles were used to remove dissolved carbon monoxide from the reaction mixture.
- a glass-lined, two-liter, stainless steel Zipperclave was charged with the following:
- the reactor and reaction mixture were purged with nitrogen.
- the reactor was pressurized to about 34.5 bar gauge (500 psig) with carbon monoxide at room temperature. Air was charged to the reactor to a total pressure of about 43.5 bar gauge (630 psig).
- the reaction temperature was brought to ca. 170°C, and the system was further pressurized to about 69 bar gauge (1000 psig) with carbon monoxide.
- the reactor was stirred under these conditions for ca. 2 hours reaction time at that temperature.
- the reactor was cooled to room temperature, and the carbon monoxide pressure vented. Nitrogen purge cycles were used to remove dissolved carbon monoxide from the reaction mixture.
- Trichloromelamine was reacted with carbon monoxide in the presence of 1-butanol at ca. 30°C for 18 hours using a catalytic quantity of an equimolar mixture of Pd(0) and PdCl 2 (at 1.5 mol% Pd on amino groups).
- a glass-lined, two-liter, stainless steel Zipperclave was charged with the following:
- the reactor and reaction mixture were purged with nitrogen.
- the reactor was pressurized to about 55.2 bar gauge (800 psig) with carbon monoxide.
- the system was stirred at ambient temperature for ca. 18 hrs.
- the carbon monoxide pressure was vented, and purge cycles using nitrogen were used to remove dissolved carbon monoxide from the reaction mixture.
- a portion (255.5g) of the neat reaction product mixture was passed through a silica gel/celite filter bed.
- the dried product (9.68g), containing the N-butoxycarbonylamino-1,3,5-triazine, was obtained by removing 1-butanol/acetonitrile from the filtrate under reduced pressure.
- a catalytic turnover number (TON) of 8.2 (mol butoxycarbonylamino groups/mol palladium) was determined from 1 H-NMR and mass spectroanalysis of the isolated product.
- Cyclohexylguanamine was contacted with carbon monoxide in the presence of 1-butanol at 170°C, and in the presence of a catalytic quantity of Pd(0) and sodium iodide. A quantity of oxygen in 20% excess over stoichiometric (on amino groups) was present.
- a glass-lined, two-liter, stainless steel Zipperclave was charged with the following:
- the reactor and reaction mixture were purged using nitrogen.
- the reactor was pressurized to about 34.5 bar gauge (500 psig) with carbon monoxide. Air was charged to the reactor to a total pressure of about 43.5 bar gauge (630 psig).
- the reaction temperature was brought to ca. 170°C, and the system was pressurized to a final pressure of about 69 bar gauge (1000 psig) with carbon monoxide.
- the system was stirred under carbon monoxide for ca. 2 hours at 170°C, followed by stirring an additional 60 hours at ambient temperature. Nitrogen purge cycles were used to remove dissolved carbon monoxide from the reaction mixture.
- N,N',N'-trichlorobenzoguanamine was reacted with carbon monoxide in the presence of 1-butanol at 90°C, and in the presence of a catalytic quantity of Ru 3 (CO) 12 .
- a glass-lined, two-liter, stainless steel Zipperclave was charged with the following:
- the reactor and reaction mixture were purged using nitrogen.
- the reactor was pressurized to about 55.2 bar gauge (800 psig) with carbon monoxide.
- the reaction temperature was brought to ca. 90°C, and the system was pressurized to a final pressure of about 69 bar gauge (1000 psig) with carbon monoxide.
- the system was stirred under carbon monoxide for ca. 18 hours at 90°C, followed by stirring an additional 3 hours at ambient temperature. Nitrogen purge cycles were used to remove dissolved carbon monoxide from the reaction mixture.
- the neat reaction mixture (83.0 g) was charged to a filtration funnel containing celite covered with a layer of silica gel.
- the dried product (2.83 g), containing the N-butoxycarbonylamino-6-phenyl-1,3,5-triazine, was obtained by removing 1-butanol from the filtrate under reduced pressure.
- a catalytic turnover number (TON) of 20.3 (mol butoxycarbonylamino groups/mol ruthenium) was determined from 1 H-NMR and mass spectroanalysis of the isolated product.
- a glass-lined, two-liter, stainless steel Zipperclave was charged with the following:
- the reactor and reaction mixture were purged using nitrogen.
- the reactor was pressurized to about 34.5 bar gauge (500 psig) with carbon monoxide. Air was charged to the reactor to a total pressure of about 43.5 bar gauge (630 psig).
- the reaction temperature was brought to ca. 150°C, followed by stirring an additional 15 hours at ambient temperature. Nitrogen purge cycles were used to remove dissolved carbon monoxide from the reaction mixture.
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Abstract
Description
at a temperature, carbon monoxide pressure, and length of time sufficient to carbonylate at least a portion of the (halo)amino groups of the 1,3,5-triazine.
Claims (16)
- A process for preparing derivatives of a (halo)amino compound comprising the step of contacting:(a) the (halo)amino compound;(b) carbon monoxide; and(c) a metal catalyst system containing a metal promoter for promoting carbonylation;
at a temperature, carbon monoxide pressure, and length of time sufficient to carbonylate at least a portion of the (halo)amino groups of the (halo)amino compound, characterized in that the (halo)amino compound is a (halo)amino group-containing 1,3,5-triazine represented by the formula: whereineach Q is independently selected from the group consisting of hydrogen and halogen, Z is a group represented by the formula -N(Q1)2,Z1 is selected from the group consisting of hydrogen, an alkyl of 1 to 20 carbon atoms, an alkenyl of 3 to 20 carbon atoms, an aryl of 6 to 20 carbon atoms, an aralkyl of 7 to 20 carbon atoms, and a group represented by the formula -N(Q1)2, andeach Q1 is independently selected from the group consisting of hydrogen, halogen, alkyl, alkenyl, aryl, aralkyl and a hydrocarbyloxy hydrocarbyl, wherein the hydrocarbyl is selected from the group consisting of alkyl, aryl, aralkyl and alkenyl. - The process of claim 1, characterized in that (a), (b) and (c) are contacted in the further presence of a hydroxy compound selected from the group consisting of straight or branched monohydric or polyhydric alkanols and alkenols having 1 to 20 carbon atoms per molecule, monohydric or polyhydric cycloalkanols and cycloalkenols having 3 to 20 carbon atoms in the molecule, monohydric and polyhydric aralalkyls having 7 to 20 carbon atoms per molecule, phenols and mixtures thereof.
- The process of claim 1, characterized in that the product is post-reacted with a hydroxy compound selected from the group consisting of straight or branched monohydric or polyhydric alkanols and alkenols having 1 to 20 carbon atoms per molecule, monohydric or polyhydric cycloalkanols and cycloalkenols having 3 to 20 carbon atoms in the molecule, monohydric and polyhydric aralalkyls having 7 to 20 carbon atoms per molecule, phenols and mixtures thereof.
- The process of one of the preceding claims, characterized in that Z1 is N(Q1)2.
- The process of one of claims 1 to 3, characterized in that Z1 is selected from the group consisting of hydrogen, an alkyl of 1 to 20 carbon atoms, an alkenyl of 3 to 20 carbon atoms, an aryl of 6 to 20 carbon atoms and an aralkyl of 7 to 20 carbon atoms.
- The process of one of the preceding claims, characterized in that each Q1 is independently selected from the group consisting of hydrogen and halogen.
- The process of any one of the preceding claims, characterized in that the metal catalyst system contains a metal promoter selected from the group consisting of a group VIII metal, a group I-B metal, a compound containing a group VIII metal, a compound containing a group I-B metal, and mixtures thereof.
- The process of claim 7, characterized in that the metal promoter is selected from the group consisting of copper, palladium, platinum, ruthenium, rhodium, compounds thereof, and mixtures thereof.
- The process of claim 8, characterized in that the metal promoter is selected from the group consisting of copper(0), palladium(0), palladium(II) chloride, palladium(II) bromide, palladium(II) acetate, palladium(II) acetyl acetonate, palladium(II) oxide, and mixtures thereof.
- The process of any one of the preceding claims, characterized in that (a), (b) and (c) are contacted in the presence of an oxidant system.
- The process of claim 10, characterized in that the oxidant system is an ingredient capable of accepting an electron from the metal promoter.
- The process of any one of the preceding claims, characterized in that (a), (b) and (c) are contacted in the presence of a hydrogen halide acceptor.
- The process of claim 12, characterized in that the hydrogen halide acceptor is a weak base.
- The process of any one of the preceding claims, characterized in that (a), (b) and (c) are contacted in the presence of a solvent.
- The process of claim 14, characterized in that the solvent comprises a nitrile solvent.
- The process of one of claims 2 or 5 to 15, characterized in that (a), (b) and (c) are contacted in the presence of a solvent comprising a combination of a nitrile solvent with a hydroxy compound selected from the group consisting of straight or branched monohydric or polyhydric alkanols and alkenols having 1 to 20 carbon atoms per molecule, monohydric or polyhydric cycloalkanols and cycloalkenols having 3 to 20 carbon atoms in the molecule, monohydric and polyhydric aralalkyls having 7 to 20 carbon atoms per molecule, phenols and mixtures thereof.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US138581 | 1993-10-15 | ||
US08/138,581 US6197957B1 (en) | 1993-10-15 | 1993-10-15 | Process for preparing derivatives of (halo)amino-1,3,5-triazines by carbonylation |
Publications (2)
Publication Number | Publication Date |
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EP0649842A1 EP0649842A1 (en) | 1995-04-26 |
EP0649842B1 true EP0649842B1 (en) | 1998-06-03 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP94116269A Expired - Lifetime EP0649842B1 (en) | 1993-10-15 | 1994-10-14 | Process for preparing derivatives of (halo)amino compounds by carbonylation |
Country Status (14)
Country | Link |
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US (1) | US6197957B1 (en) |
EP (1) | EP0649842B1 (en) |
JP (1) | JP4039702B2 (en) |
AT (1) | ATE166871T1 (en) |
AU (1) | AU678851B2 (en) |
BR (1) | BR9404093A (en) |
CA (1) | CA2118073A1 (en) |
DE (1) | DE69410738T2 (en) |
DK (1) | DK0649842T3 (en) |
ES (1) | ES2117185T3 (en) |
GR (1) | GR3027780T3 (en) |
MX (1) | MX196675B (en) |
NO (1) | NO305983B1 (en) |
TW (1) | TW358092B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0847417B1 (en) * | 1995-08-30 | 2004-11-24 | Cytec Technology Corp. | Compositions containing 1,3,5-triazine carbamates and epoxy compounds |
CA2247905A1 (en) * | 1996-03-01 | 1997-09-04 | Lon-Tang Wilson Lin | Cyclic imido-1,3,5-triazine crosslinking agents |
US6121446A (en) * | 1998-11-10 | 2000-09-19 | Cytec Technology Corporation | Preparation of tris-substituted alkoxycarbonylamino-1,3,5-triazine compounds |
US7399841B1 (en) | 2005-09-15 | 2008-07-15 | The United States Of America As Represented By The Secretary Of The Navy | High-energy 1,3,5-triazinyl diazenes, and process thereof |
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US3641092A (en) | 1966-11-25 | 1972-02-08 | Hercules Inc | Isocyanate synthesis from amines and carbon monoxide catalyzed by pdcl2 |
EP0083096B1 (en) | 1981-12-25 | 1987-02-25 | Asahi Kasei Kogyo Kabushiki Kaisha | Production of urethane compounds |
US5068424A (en) | 1988-06-17 | 1991-11-26 | Nitrokemia Ipartelepek | Process for preparing arylsulphonyl-isocyanates and addition derivatives thereof |
US5008435A (en) | 1988-11-22 | 1991-04-16 | Industrial Technology Research Institute | Preparation of urethanes |
US5084541A (en) | 1988-12-19 | 1992-01-28 | American Cyanamid Company | Triazine crosslinking agents and curable compositions |
US4939213A (en) | 1988-12-19 | 1990-07-03 | American Cyanamid Company | Triazine crosslinking agents and curable compositions containing the same |
US5194660A (en) | 1990-12-21 | 1993-03-16 | Union Carbide Chemicals & Plastics Technology Corporation | Processes for producing carbamates and isocyanates |
US5288865A (en) * | 1991-11-15 | 1994-02-22 | American Cyanamid Company | Process for preparing amide derivatives from haloaminotriazines and acid halides |
-
1993
- 1993-10-15 US US08/138,581 patent/US6197957B1/en not_active Expired - Lifetime
-
1994
- 1994-09-07 TW TW83108256A patent/TW358092B/en active
- 1994-10-11 JP JP27169994A patent/JP4039702B2/en not_active Expired - Lifetime
- 1994-10-13 CA CA002118073A patent/CA2118073A1/en not_active Abandoned
- 1994-10-14 MX MX9407977A patent/MX196675B/en unknown
- 1994-10-14 DE DE69410738T patent/DE69410738T2/en not_active Expired - Lifetime
- 1994-10-14 NO NO943908A patent/NO305983B1/en not_active IP Right Cessation
- 1994-10-14 ES ES94116269T patent/ES2117185T3/en not_active Expired - Lifetime
- 1994-10-14 BR BR9404093A patent/BR9404093A/en not_active IP Right Cessation
- 1994-10-14 EP EP94116269A patent/EP0649842B1/en not_active Expired - Lifetime
- 1994-10-14 AT AT94116269T patent/ATE166871T1/en active
- 1994-10-14 DK DK94116269T patent/DK0649842T3/en active
- 1994-10-14 AU AU75836/94A patent/AU678851B2/en not_active Ceased
-
1998
- 1998-08-31 GR GR980401958T patent/GR3027780T3/en unknown
Also Published As
Publication number | Publication date |
---|---|
CA2118073A1 (en) | 1995-04-16 |
DE69410738T2 (en) | 1999-01-14 |
US6197957B1 (en) | 2001-03-06 |
ATE166871T1 (en) | 1998-06-15 |
NO943908D0 (en) | 1994-10-14 |
NO943908L (en) | 1995-04-18 |
AU678851B2 (en) | 1997-06-12 |
GR3027780T3 (en) | 1998-11-30 |
BR9404093A (en) | 1995-06-13 |
TW358092B (en) | 1999-05-11 |
EP0649842A1 (en) | 1995-04-26 |
JP4039702B2 (en) | 2008-01-30 |
MX196675B (en) | 2000-05-30 |
DK0649842T3 (en) | 1998-10-12 |
JPH07188194A (en) | 1995-07-25 |
AU7583694A (en) | 1995-05-04 |
ES2117185T3 (en) | 1998-08-01 |
NO305983B1 (en) | 1999-08-30 |
DE69410738D1 (en) | 1998-07-09 |
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